Method of generating and utilizing motive fluids.



E. 61 W. H. TAYLOR.

METHOD OF GENERATING AND UTILIZING MOTIVE FLUIDS.

APPLICATION FILED nun: \1. 1912.

1,241,781 Patent/ed Oct-2,1917.

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E. & W. H. TAYLOR.

METHOD OF GENERATING AND UTILIZING MOTIVE FLUIDS.

APPLICATION FILED JUNE I7 I9l2.

1,241,781. Patented 00th 2,1917.

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E. 5: W. H. TAYLOR. METHOD OF GENERATING ANd UTILIZING MOTIVE FLUIDS- APPLICATION FILED JUNE 11. m2.

1,241,781 Patented Oct. 2,1917.

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APPLICATION FILED MINE H, l9l2. 1,241,781. Patented Oct. 2,1917.

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E. 61 W. H. TAYLOR.

METHOD OF GENERATING AND UTILIZING MOTIVE FLUIDS.

APPLICATION mm JUNE 11. I912.

1,241,781. Patented Oct. 2,1917.

6 SHEETS-SHEET 5.

E. & W.-H. TAYLOR. METHOD OF GENERATING AND- UTILIZING MOTH/E FLUIDS.

APPLICATION FILED JUNE I], 1912- 1,241,781 Patented Oct. 2,1917.

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UNITED STATES IEXTENT OFFICE.

ED'WIN TAYLOR AND WILLIAM H. TAYLOR, OF NEW YORK, N. Y., ASSIGNORS, BY MESNE ASSIGNMENTS, TO TAYLOR-HUBBARD COMPANY, A CORPORATION OF NEW YORK.

METHOD OF GENERATING AND UTILIZING MOTIVE FLUIDS.

Specification of Letters Patent.

Patented Oct. 2, 191 '7.

Application filed June 17, 1912. Serial No. 704,055.

To all whom it may concern:

Be it known that we, EDWIN TAYLOR and WILLIAM H. TAYLOR, citizens of the United States, and residents of the city of New York, in the county of New York and State of New York, have invented certaln new and useful Improvements in Methods of Generating and Utilizing Motlve Flulds, of which the following is a speclficatlon.

One of the chief problems in modern technics is the generation of power W1th an economic use of fuel and as small as possible waste of heat. This waste exists in steam as well as hydrocarbon engine practice. It is a well known fact that not more than twelve per cent. of the cost of fuel is converted into actual work. Numerous efiorts have been made to find a substitute for coal or for the more expensive hydrocarbons, and crude petroleum, articularly Mexican 011, has been suggested without, however, having ever been utilized for the production of motive fluid to any considerable extent.

The principal object of the present invention is to provide a method of generating motive fluids from hydrocarbons, whereby the loss in heat efiiciency, heretofore experienced, is greatly reduced, it being well known that by prior methods and apparatus, the major,portion of the products of combustion of the combustible materials used, are drawn u the stack or otherwise lost, without per orming any mechanical work.

Another object of this invention is to provide a method whereby it is possible to utilize a relatively low grade, and consequently low priced, fuel, such as crude petroleum or Mexican oil, which is rich in tarry substances, and has heretofore been regarded as nearly incapable .of bein used for power generating purposes. Sue oils may be used either alone or in the presence of other fuel, such as coal.

It is another object of this invention to in crease the efl'ective utility of the products of combustion of carbonaceous materials, simply for heating purposes or, expansively or otherwise, for doing work in a prime mover.

Another object of this invention is the saving and using over of the products of combustion, for example, the water produced by the combustion carbons.

The invention has been embodied in an apparatus for generating and utilizin motive fluids for which application for S. Letters Patent has been made, Serial No. 653,608 filed October 9, 1911, and the methods used therein and forming the subject-matter of the present application, are illustrated in the accompanying drawings, in which,-

Figure 1 is a diagrammatic view of the action of a fuel jet and a water jet, contacting at an acute angle,

Fig. 2 is a similar view of the action of the jets, arranged concentrically to each other and coaxially to the generating chamber,

Figs. 3 and 4 are similar views, at right angles to each other, respectively, of the action of the jets, arranged tangentially to the axis of the generating chamber,

Fig. 5 is a similar view of the action of the jets arranged coaxially opposing each other and representing the preferred form of the present invention.

Fig. 6 is a similar view of the action of a p lura5lity of jets, arranged analogous to Fig. 7 is a cross sectional view of Fig. 6 in the plane of impact of the jets,

Fig. 8 is a front elevation, partly diagrammatic, of an apparatusembodying the present invention, and

Fig. 9 is a side elevation shown in Fig. 8.

The method of generatin a motive fluid to accomplish the objects 0 the present invention consists in projecting a jet of inflammable material in a state of ignition into a suitable space, and mixing it therein with air, water or other oxygen-bearing fluids. The rojection of the jet of inflammable material takes place in the form of a heat-generating cone which contacts with or is opposed by a similar cone of oxygen-bean ing material, forming a heat-absorb1ng cone. The projection of these cones into a confined space results in an approximate plane of contact or impact, and, in its preferred of the apparatus of liquid hydro-- form, when the projecting cones are coaxially op osing each other, in a plane of impact su tantlally at right angles to the axes and approximately midway between the apices of the cones and preferably of a diameter less than that of the confined s ace.

The products of combustion escape rom the confined space through suitable openings with a swirlin movement causing a complete mixture, 0 uniform temperature, of the different gaseous substances. The apparatus used in carrying out the methods of the present invention are instrumental in obtainlng a series of cycles that ultimately result in motive power and comprise, in constant rotation and the same sequence, first, ignition, second, combustion third, expanslon, fourth, propulsion, fift ,exhaust and sixth, condensation.

The effective use of this series of cycles results in the utilization of the so far hi hest ercentage of heat units from the uel use including all those from the gaseous products of combustion as well as the aqueous vapor produced by combustion. The products resulting from the contact of the heat-generating jet and the heat absorbing jet form a uni ormlymixed compound fiui of any desired temperature and pressure which, expansively or otherwise, can be used in prime movers such as steam engines or other motors. The pressures and temperatures of the fluids depend upon the relative proportions of the heat-generatin and heatabsorbing jets and can be vari by either diminishing the heat-generating et and holding the'heat-absorbing jet constant or vice versa.

The form and size of. the injecting nozzles is of time importance and they should prefera ly be dissimilar. The tendency to expand of the products of combustlon of the heat-generating jet is different from that of the heat-absorblng jet and this results in the formation of a clrcle of larger diameter at any given distance from the nozzle of the heat-generating jet than that formed by the opposing heat-absorbing jet at an' equal distance. It is important, therefore, that the areas of the o posing cones at the plane of impact shou d be circles of the same diameter.

For the generation of large powers, however, a plurality of opposed jets may be used, the axes of which should be parallel. The op osing cones are so spaced apart that their planes of impact areequal and equi; distant from the ets and the sum of the diameter of the planes of impact, smaller than the diameter-of the generating chamber. While the preferred arrangement consists in having all heat-generating cones located on one side of the chamber and the heat-absorbing cones on the opposite side. they may also be arranged by having part of the heat-generatingand heat-absorbing cones on one side and a similar arrangement on the opposite side.

A varlety of fuels, such as gas, oil, crude petroleum; chemicals, powered carbon, &c., may be employed for the heat-generating cone, while water or various chemicals, such as sulfurlc acid, &c., or other hydrogenous materlals may be employed in the heatabsorbing cone. The necessary oxygen may be taken from the atmosphere or furnished by introducing various oxygen-producing compounds.

As already stated hereinbefore, while the use of an air and fuel jet, supplemented by a et of water, is old in the art, the use of a fuel et and water jet in a confined space and so arranged that the products of combustlon of the fuel jet are opposed by the water et, and the mixed products permitted to escape from the generating space at a unlform temperature and with a swirling mot on, to be subsequently expanded in an englne cylinder, is thought to be broadly new and forms the essence of generating motlve fluid from fuel, according to the resent invention. The use of crfide petroeum, such as Mexican oil, containing a large percentage of tarry matter, is one of the partlcular advantages obtained by these methods. I 7

It has been found that the rate of combustlon of oil is directly dependent upon the pressure in the generating chamber, and that a particle of oi too large to burn completely under atmospheric pressure, will burn completel under pressure greater than atmospheric. or instance, a particle of oil of certam volume, under one hundred pounds pressure will be burned in about one-third of the time requlred for burning a similar pai'ticle iii the 0 on air;

n app ying t is princi le to en e rac two, it has been found th at when tl l esd oils are burneddirectly in an engine cylinder, the depositlon of tar, &c., as solid matter 1s ncreased-owing to the cold walls with whlch the oil is in contact before combustion 1s complete. This obviously causes gummmg and sticking of the pistons and finally stoppa of the engine. In the present metho .of utihzing oils, this do sition of tarry matter is practically eliminated, owmg to the high rate and perfection of combustion, so that only a small amount of solid tarry substance is formed, which is revented from adhering to the cylinder w s, by the large volume of aqueous. vapor and is washed off as rapidly as it is formed.

The theo of the action of fuel and water, as used in t e present invention, is com reiiensi yely illustrated in the drawings, igs.

0 indicates the heat-generating jet.

W indicates the heat-absorbing-jet.

B represents the zone of partial mixture and high super-heat.

C represents the zone of aqueous va partially heated by radiant heat, which increases toward the zone D.

D represents the zone of mixture and expansion and the products of combustion in this zone have developed a swirling or rotary motion.

E represents the zone of complete combustion at a maximum temperature.

F represents the zone of inactive gas and va or,

are the outlet orifices,

H the axes of direction of the jets,

J the lane of impact,

K the insulating jacket, and

L the water jacket.

In Fig. 1 of the drawings, the heatenerating jet approaches the heat-absor ing jet at an acute angle and it is obvious that the products of combustion of the heat-generating jet are considerably cooled on the side of im act with the heat-absorbing jet and, therei bre, produce incomplete combustion throughout the plane of impact. As it were, the oil particles of the heat-generating jet are met and extinguished by an overwhelming amount of Water before their combustion. This results obviously in the formation of lar e amounts of carbon monoxid CO instead 0% carbon dioxid C0,, the product of complete combustion. The sudden cooling of the hydrocarbon flame of the heat-generating jet, causes also the formation of large amounts of soot. The temperature at the plane of impact of flame and water, however, is apparently still sufficient to disassociate the oxygen and hydrogen of the water, causin therefore, a consequent absorption of eat. It is doubtful whether this heat so absorbed is subsequently again released, inasmuch as the oxygen and hydrogen so produced are rapidly cooled by the incoming heat-absorbing jet and may never become hot enough to again confine and again liberate the absorbed heat.

Fig.2 illustrates the action of jets ar-. ranged coaxially and concentrically and, since the heat-absorbing jet completely surrounds the heat-generating jet, it is obvious that this entire form should be completely insulated, as indicated at K, to confine the heat, instead of being water-jacketed to lead off the heat.

Figs. 3 and 4, illustrating tangentially arranged jets show that the swirling motion of the gases and vapors be ins a most on leaving the jets. The heat oss in this arrangement is greater than that of the arran ment shown in Fig. 1, on account of the liiirning gases being in contact with the cold walls of the generator and the entering water for a longer time and greater distance. The compartment, therefore, is prefor, eat

erably insulated as shown at K. A bafile plate M may be employed to prevent the extinguishing of the heat-generating jet 0, by means of the heat-absorbing jet.

Fig. 5 illustrates the preferred form of the present invention, in which the heatenerating jet is coaxially opposed by the ieat-absorbing jet. One of the distinctive features of this arrangement is the absence of the zone A, e. the zone of incomplete combustion and heat loss.

In the present method, the heat-generating material and the heat-absorbing ma-' terial are driven through their orifices and into impact with one another by compressed air, exerting a constant pressure and carrying the fue and water to the 'ets and mixing and atomizing the same t ere. to form a properly combustible mixture and a propor y expanslve vapor, each developed into a cone projected into the chamber until they meet in the plane of impact.

In this form the heat-generating and heatabsorbing jets or fuel jet and Water jet, as they may be called, enter the confined space or combustion chamber coaxially from opposite points. The orifices or nozzles are so designed that the burning hydrocarbons and the spray of water, are opposing each other in the shape of cones, in which the plane of impact formed by the basis of the cones, is approximately circular and located at or near the center of the generating chamber. As heretofore stated, the diameter of the area of impact can obviously be regulated by the force of the entering jets and should preferably be smaller than the diameter of the chamber, so as to leave a space filled with superheated vapor and gas, between the cones and the walls of the combustion chamber. This arrangement prevents considerably the loss of heat by radiation or by the contact of the products of combustion with the walls of the generating chamber.

An important element in the arrangement shown in Fig. 5 is the angle of dispersion of the jets. As stated before, the diameter of the area of impact, should always be less than that of the generating chamber, so as to permit the products of combustion to assume a swirling or rotary movement at the periphery of the plane of impact and to cause these vapors to become practically of a uniform mixture and temperature before they escape through the orifices G to the point of utilization.

Fig. 5 also illustrates the advantage of employing dissimilar nozzles for the entering jets. This is necessitated by the fact that the heat generating jet, emanating from the nozzle 0, expands adiabatically, while the heat absorbin jet, emanating from the nozzle W, expan s uniformly. The heatgenerating cone, therefore, should have a smaller angle of entrance than the heat-absorbing cone. This arrangement results in perfect and uniform combustion, inasmuch as all of the products have an equal amount of time and distance in which to complete their burning and are not subjected to extreme outside cooling efi'ects before they reach the plane of impact. The presence of a volume of super-heated vapors and gases, swirling around the cone of the heat-absorbing jet within the walls of the generating chamber, prevents the depositing on the walls thereof, of aqueous vapor and the flooding by water of the bottom of the chamher.

The products of combustion, however, forming the cone E of the heat-generating jet, are prevented from comin in contact with the walls of the generator y a volume D of super-heated gases and vapors which tends to insulate the cone E from the walls of the generator and thus permits a maximum heating and combustion in the cone and a minimum loss b radiation through the generator walls. his heat loss is still further reduced by means of the water jacket L, surrounding that part of the generating chamber which incloses the heat-generating jet, and the heat that passes through the generator walls, is absorbed by the water jacket and returned to the chamber through the heat-absorbing 'et W,

It is thought to e radically new in the art, to water-jacket the side of the generating chamber, surrounding the heat-generating cone making the same thereby impervious to the eflects of high heat, insulating the sides of the generator at the opposite end and then returning, both the heat and the water, to the generating chamber by means of the heat-absorbing cone. The side of the generating chamber, surrounding the heat-absorbing cone, is insulated as at K, to prevent the gases swirlin around this cone, to become unduly coole by con tact with the generator walls. It must be evident that the heat .eflect on the side of the chamber, which surrounds the heat-generating cone, must be far greater than that on the side of the heat-absorbing cone, therefore, the water jacket L is provided on one side and the insulation K on the other.

Figs. 6 and 7 are analogous in arrangement to Fig. 5, except that a plurality of jets are provided, increasing the capacity of the device enormously. This arrangement has the additional advantage that the pressure and volume of the issuing gases and vapors can be controlled by igniting or extinguishing any desired number of the same, and observation ports W (Fi 7), are provided, so that the internal con itions of the enerating chamber may be readil observed and the operation of each individ ual nozzle controlled at will.

diate method, in which the water to be en plied to the air compressor, is carried irectly to the valve of the same and there atomized by the incoming air and held suspended in the compressing chamber to absorb the heat of compression, as it develops. This heated water thereafter is ejected in a state of steam, together with the issuing air, and the portion that remains fluid or condenses in transit, is led to the water jacket of the generator while that which remains as vapor, enters the jet of the heat-absorbing cone and it will be seen therefrom that all the heat of compression is utilized in the generator chamber.

Inasmuch as air pressure has a direct bearing upon combustionthe rate of combustion doubling with the pressure-the air is injected into the generating chamber at as high a temperature as the working con ditions will permit and it thereby serves in returning heat units, produced in the air compressor, to the generator chamber with a corresponding increase in efliciency. The compressed air, entering the combustion chamber, is increased to more than double its volume by the heat transmitted to it by the generator, and thereby becomes adapted to perform work additional to that required in com ressing it. If now by the introduction 0 water, the gases in the generating chamber are cooled the heat ciency is considerably lowered, but it must be remembered that, inasmuch as in the present method the issuing gases can be utillzed at a considerable low temperature, at about 800 Fahrenheit, while the jets are operated at about 3000 Fahrenheit, it can readily be understood that the actual thermal efliciency of the resent method is very high, the net result eing a considerable gain over the usual type of internal combustion engines and far superior to any steam engine, the reliability and flexibility of which, however, is retained in addition to the elimination of the ignition, carbonation &c. of the gas en- The theoretical efliciency of the present method is largely influenced by the quality of fluid, introduced as the heat-absorbing jet. Water is preferabl used for this purpose, because it has no ad efiect upon the workin parts, maintains heat efiiciency and, particu arly because the combustion of any ydrogen-containinglfuel, results in the production of water w ich may a ain be utilized in succeeding cycles, and orms one of the most important and distinctive features of the present method. A moderate supply of water is only required and, as a matter of fact, at the end of a period of operations under the present method, there should be more water in the machine than there was at the start.

The expansive gases produced in the generator, are directly led from there to the cylinder of an engine or other prime mover or they may be used for heating purposes, for which otherwise heated steam is used, such as in heating of houses, steam tables &c.

They consist mostly of carbon dioxid and nitrogen, mixed with highly superheated agueous vapor. 0

out inventions, may be used in connection with any ordinary ty e of engine, pump or motor. Since one of the main objects of these methods is the utilization of heat units 1 and the prevention of waste, the exhaust gases and vapors, leaving the engine or other device of utilization, are'suitably controlled and led to a condenser, where the vapors are condensed and returned to the generator, while the noncondensable gases, carbon dioxygen and nitrogen, for instance, escape into the atmosphere.

The water, formed in the condenser, is conveyed by gravity or otherwise, to theair compressor and is there atomized by the incoming air, absorbs the heat, developed on the heat compression stroke and is then again changed to steam. The air also.carrice the water which has condensed, after leaving the compressor and which has not vaporized in the compressor, through a suitable trap or separator, where the bulk of it is separated from the air, while the small amount of vapor, passing through with the air, will again be utilized in the heat-generating and heat-absorbing cones. The water from the separator is forced into the water jacket of the generator, heated therein and passedofi' into the generator chamber by means of the nozzle of the heat-absorbing cone, while, similarly, the fuel is pumped from the fuel reservoir into the generator by means of the nozzle of the heat-generat ing cone. In the generator chamber, the fuel jet once ignited burns continuously, the water jet enters continuously from the opposite nozzle, mingling with and cooling the roducts of combustion and forming a liighly expansive body which is conducted to an engine or other device, where it per forms its work and again enters the condenser to be prepared for another continuous cycle of ignition, combustion, expansion, propulsion, exhaust and condensation, utilizing a maximum of heat units to the greatest advantage as hereinbefore already set forth.

One form of an apparatus for employing the present invention is illustrated in Figs. 8 and 9 shown as secured to a side wall A, by means of the wall base plate B, and the It is evident that the meth s, forming the subject-matter of the presscrew bolts C, and comprises an air compressor 1, a condenser 2, having an exhaust pipe 3, communicating with the atmosphere, and a connecting pi e 4, leadin from the condenser to the in ct valve -0 the compressor. The compressor is connected by a pipe line 5 to an air receiver 6.

A fuel tank 7 contains the necessary oil, petroleum, etc. and a water tank 8 a suitable supply of water, which both are led to a suitable generator, indicated at 9, by means of a pipe line 10 establishing connection between the generator and the fuel tank, and another pipe line 11, between the generator and the water tank. A water nozzle, the inlet for the heat-absorbing jet, is shown at 12 and a fuel nozzle, the inlet for the heatenerating jet, at 13. A valve 14, on top 0 the generator 9 may be used as starting and igniting means and is opened by hand, to let the products of combustion escape into the open air, until the fuel jet is full started. A valve 15 in the pipe 16 contro s the supply of compressed air from the air receiver 6 to the water nozzle 12 and a similar valve 17 in the pipe 18 the supply of air to the fuel nozzle 13.

The fuel jet side of the generator is provided with a water jacket 19, which receives its water through the pipe line 11 and gives it off to the water jet through the nozzle 12. The water jet side of the generator is provided with a heat insulating filling 20. The purpose of the water jacket is to absorb the heat of combustion, while that of the insulating filling is to prevent loss of heat by radiation. An electric spark or igniting plug 21 ma be arranged on the generator instead of the valve 14, for igniting the fuel jet and a hand operated air pump 22 may be used to establish the initial air pressure in the air receiver. v

The motive fluids produced in the erator are carried off, by means of a main 23 (wherein is placed a reducing valve 23), which is by-passed at 24 to the air com pressor, and receives back the part of the motive fluids, used in the compressor, through the pipe 25. A pipe line 26 finally supplies the motive fluids to a prime mover 27, where they are utilized and exhausted through the plpe 28 to the condenser 2.

The operation of an a paratus for carrying out the methods or generating and utilizing motive fluids, such as illustrated in Figs. 8 and 9, is as follows ssuming that the apparatus has not yet been used, water is admitted to the water jacket 19 of the generator 9 from the water reservoir 8 through the pipes 11. The hand air pump 22 is then started and air under pressure supplied to the air receiver 6. Fuel IS supplied from the fuel reservoir 7 through the pipe 10 to the fuel nozzle 13, the valve 17 in the p p 8 is hen opened and with gen- Qua

the valve 14 open, air supplied to the fuel nozzle, causing the fuel to enter the e rator, finely divided and atomized, w erem it is ignited by means of the spark plu 21.

After the flame of the fuel nozzle is y started and regulated, the valve 15 in the pipe 16 is opened and compressed air is supplied to the water nozzle 12, causing a finely divided spra of water to op ose and impact upon the ame of the fue nozzle. Compressed air is still supplied by hand until the two opposin cones, the heat-generating jet of the fue nozzle and the heatabsorbing jet of the water nozzle, are fully developed and properly ad usted, whereupon the valve 14 1s closed.

The pressure of the mot ve fluids, now generated in the generator, rises slowly until it is suflicient to pass through the mam 23 and the by-pass 24 to the com ressor 1 and to operate the same, from who time, the operation of the entire apparatus becomes entirely automatic. The pressure in the genorator increases further until it is capable to operate the prime mover 2 7, wherein the motive fluids are utilized, giving ofl their exhaust gases to the condenser 2, where the aqueous constituents are cooled and transformed into water for renewed use, while the. carbon dioxid and nitrogen escape mto the atmosphere, in this manner completm the entire cycle of operation, the essence o the present invention.

Claims: 1

1. The method of generating motive fluids which consists in opposing m a confined space, currents under pressure, of heat generating fluids aided in, and heat absorbing fluids refrained from dispersing heat.

2. The method of generating motive fluids which consists in directing a current of combustible fluid aided in dispersing heat, against a current of expansible fluid refrained from dispersing eat, and causing combustion of the commingling fluids 3. The method of enerating motive fluids which consists in directing a current of combustible fluid aided in dis ersing heat, against a current of expansi le fluid refrained from dispersing heat, causing combustion of the commingling fluids, and utilizin the products of said combustion.

4. he method of generating motive fluids which consists in separately atomizing heat generating and heat absorbing materials, aiding said heat generating materials in and refraining said heat absorbing materials from dispersing heat, and causing said materials to contact under pressure at temperature of combustion.

5. The method of generating motive fluids which consists in separately atomiz ing heat generating and heat absorbing materials, aiding said heat generating materials in and refraining said heat absorbing materials from dispersing heat, causing said materials to contact under ressure at temperature of combustion, an utilizing the products of said combustion.

6. The method of generating motive fluids, which consists in opposing in a confined space a jet of inflammable mate l in a state of combustion to a jet of bee absorbing material, utilizing the fluids so obtained, condensing the aqueous products of combustion from said fluids, and returning.

thel same to said jet of heat-absorbing mate- 113- 7. The method of generating motive fluids which consists in opposing in a confined space a jet of inflammable material in a state of combustion to a jet of heat absorbing material aiding said jet of inflammable material in and refrainin said jet of heat absorbin material from dispersing heat, utilizing t e' products so obtained, condensing the aqueous constituents thereof, and returning the same to said jet of heat absorbing material.

8. The method of generating motive fluids which consists in opposing in a con: fined space, currents under pressure, of heat generating fluids aided in dis ersing heat, and heat absorbing fluids re ained from dispersing heat, causing combustion of the commingling fluids, utilizing the products of said combustion, condensing the aqueous constituents thereof, and returning the same to said current of heat absorbing fluids.

9. The method of generating motive fluids which consists in opposing in a confined space two or more currents of heated fluids containing oxygen-bearing material, one or more of aid currents eing in a state of combustion and aided in dispersing heat, said currents meeting in a plane of impact of an area less than that of said confined space in said plane.

10. The method of generating motive fluids which consists in causing combustion in a confined space of opposing jets of similar area of impact, of eat generating and heat absorbing fluids under pressure, simultaneously therewith preheating said heat absorbing fluids by the ignited jet of said heat generating fluids, and then utilizing the products of combustion for the translation of energy.

11. The method of generating motive fluids which consists in projecting into a confined space, opposing jets under pressure of fluids containing oxygen bearing materials, one of said jets in a state of combustion impacting upon the other, the latter consisting in part of products of combustion formed by a previous impact of said jets.

12. The method of generating motive fluids which consists in projecting into a confined space from opposite directions heat-generating and heat-absorbing cones, the axes of said cones coinciding with that of said space, and the area of impact of said cones being less than that of said confined space in said plane of impact, conveying off the fluids produced by said impact to utilize the same, condensing the aqueous constituents from said fluids, and returning the same to said heat-absorbing cone.

13. The method of generating motive fluids which consists in opposing in a confined space, currents under pressure of heat generating and heat absorbing fluids, causing combustion of the commin ling fluids, leading off the products of com ustion, bypassing a portion thereof for the translation of ener to cause said pressure, returning said y-passed portion to the remaining Portion, and then utilizing both portions or the translation of energy.

14. The method of generating motive fluids which consists in opposing in a confined space, currents under ressure of heat generating and heat absorbln fluids, causing combustion of the'commingling fluids, leading off the products of combustion, bypassing a portion thereof for the translation of energy to cause said pressure, returning said by-passed portion to the remaining portion, utilizing both portions for the translation of energy, condensing the aqueous constituents of the united portions and returning the same to said current of heat absorbing fluids.

15. The method of generating motive fluids which consists in opposing 1n a confined space, currents under pressure and of substantially equal area of impact, of heat generatin and heat absorbing fluids, the first aide in and the latter re rained from dispersing heat.

16. The method of fluids which consists in irecting a current of combustible fluid against a current of expansible fluid, the first aided in and the latter refrained from dispersing heat, both currents meeting with substantially equal area in the plane of impact, and subjecting the commingling fluids to the action of combustion.

17. The method of generating motive fluids which consists in separately atomizing heat generating and heat absorbing materials, the first aided in and the latter refrained from dispersing heat, and causing said atomized materials to contact with substantially equal area under pressure in a plane of impact and at temperature of comustion.

18. The method of generating motive fluids which consists in separately atomizing heat generating and heat absorbing materials, the first aided in and the latter reenerating motive frained from dispersing heat, causing currents of said materials to impact upon each other with substantially equal area in a confined space, and maintainmg in said space temperature of combustion.

19. The method of generating motive fluids which consists in opposing in a con-' fined space a 'et of inflammable material in a state of com ustion to a jet of heat absorbing material, the first aided in and the latter refrained from dispersing heat, said jets meeting with substantially equal area of impact, and conveying oil the fluids so obtained to a point of utilization.

20. The method of generating motive fluids which consists in opposing in a confined space, currents under pressure of heat generating and heat absorbing fluids, utilizing the resulting fluids, condensing the aqueous constituents thereof, and returning the same to said confined space.

21. The method of generating motive fluids which consists in opposing in a confined space, currents under pressure, of heat generating fluids aided in, and heat absorbing fluids containing hydrogen and oxygen in a proportion to form water, and refrained from dispersing heat.

22. The method of enerating motive fluids which consists in irecting a current of combustible fluid aided in dispersin heat, against a current of expansible flui containing hydrogen and oxygen in a proportion to form water, and refrained from dispersing heat, and causing combustion of the comminglin fluids.

23. The met 0d of generating motive fluids which consists in separatel atomizing heat generating materials an heat absorbing materials containing hydrogen and oxygen in a' proportion to form water, aiding said heat generatin materials in and refrainin said heat aflsorbing materials from dispersing heat, causing said materials to contact under pressure at temperature of combustion, and utilizing the products of said combustion.

24. The method of generating motive fluids which consists in opposingin a confined space currents under pressure, of heat generating and heat absorbing fluids, causing combustion of the commin lin fluids, leading oil the products of com ustion, bypassing a portion thereof for the translation of energy to cause said ressure, and utiliz ing the remaining portlon for the translation of energy for other purposes.

25. The method of generating motive fluids which consists in opposing in a confined space currents under pressure, of heat generating and heat absorbing fluids, causing combustion of the commmgling fluids, leading off the products of combustion for the translation of ener to cause said pressure and thereafter ut1 izing said products of combustion for the translation of energy ing the same to said current of heat absorbfor other purposes. fluids. 15 26. The method of generating motive n witness whereof the inventors have fluids which consists in opposing m a conhereunto set their hands in the presence of fined space currents under pressure of heat two subscribing witn I i a at Philadelphia generating and heat absorbmg fluids, causin the county of Philadelphia and State oi mg combustion of the commm ling fluids, Pennsylvania, this 10th day of June, 1912. 20

leading 05 the products of com ustion for EDWIN TAYLOR v the translation of energy to cause said pressure, and thenutilizing them for the trans- WILLIAM TAYLOR- lation of energy for other purposes con- In presence of densing the aqueous constituents of the re- P. S. PARIS u maining products of combustion and return- 'Trmo. H. Cnm. 

